Positive active material for lithium rechargeable battery, manufacturing method thereof, and lithium rechargeable battery including same positive active material

ABSTRACT

The present disclosure relates to a positive active material for a lithium rechargeable battery, a manufacturing method thereof, and a lithium rechargeable battery including the positive active material, and it provides a positive active material which is a lithium composite metal oxide including nickel, cobalt, and manganese, and either has orientation in a direction of [001] with respect to an ND axis that is equal to or greater than 29% or has orientation in a direction of [120]+[210] with respect to an RD axis that is equal to or greater than 82% in the case of an EBSD analysis with a misorientation angle (Δg) that is equal to or less than 30 degrees.

CROSS-REFERENCE TO RELATED APPLICATION

This application claims priority to and the benefit of Korean Patent Application No. 10-2017-0177562 filed in the Korean Intellectual Property Office on Dec. 21, 2017, the entire contents of which are incorporated herein by reference.

BACKGROUND OF THE INVENTION (a) Field of the Invention

The present disclosure relates to a positive active material for a lithium rechargeable battery, a manufacturing method thereof, and a lithium rechargeable battery including the positive active material.

(b) Description of the Related Art

A positive active material that is one of elements configuring a lithium rechargeable battery directly serves in realization of energy density of the battery, and also becomes a factor in determining a life-span characteristic. In relation to this, researches on ternary positive active materials bases on nickel, cobalt, and manganese have recently been in active progress, and are mainly used to manufacture a positive electrode precursor using a co-precipitation method. The manufacturing of a ternary positive electrode precursor using a co-precipitation method signifies a method for injecting nickel sulfate, cobalt sulfate, and cobalt manganese in a 1-3M concentration into a reactor, and performing co-precipitation by using an ammonia solution as a complexing agent and caustic soda as a precipitator. The above information disclosed in this Background section is only for enhancement of understanding of the background of the invention, and therefore it may contain information that does not form the prior art that is already known in this country to a person of ordinary skill in the art.

SUMMARY OF THE INVENTION

Providing orientation to a precursor for a ternary positive electrode material used in the lithium rechargeable battery is generally known to mostly produce excellent electrochemical characteristics such as capacity, rate control, or cycle lifespan compared to a positive electrode material with no orientation, as a c-axis direction is perpendicularly arranged with respect to a direction in which lithium is intercalated or de-intercalated.

However, the precursor to which orientation is provided is known to be realized only when a concentration gradient is given to the precursor, and the concentration of metal ions in an inflow tank must change in order to realize this, so only batch-based process driving is allowable.

Further, to realize the batch process, a plurality of influent tanks for configuring a core and a shell are needed. Therefore, the method for assigning orientation in prior art has a drawback of high processing costs, compared to the general precursor manufacturing process.

The present invention realizes the orientation that is realizable in the conventional batch reactor in a flow reactor to thereby implement a skill for manufacturing a positive electrode precursor with orientation when there is no concentration gradient.

The discovery that a positive electrode material with orientation is possible through a concentration gradient represents an approach based on realizing experience-based orientation.

The present inventor analyzed the effect of the concentration gradient on formation of the precursor to deduce an effect for providing orientation of the precursor when there is no concentration gradient.

While the conventional general method for assigning orientation represents a method for forming a precursor by changing a concentration of metal ions that are input when a co-precipitation precursor is manufactured, the present invention relates to a method for assigning orientation not by changing the concentration of metal ions but by changing a process variable.

When the orientation is assigned by changing the process variable, a batch-type process used for assigning orientation in conventional art may be changed to a flow process, thereby generating an advantage of substantially reducing production cost of the precursor. In addition, in the case of applying it to the batch process, the manufacturing cost is reduced and no precise composition control is needed by reducing at least two types of inflow tanks for controlling the concentration of metal ions that are an influent to one type, so time control and pump control for manufacturing an oriented precursor may be simplified.

The present invention proposes a skill for manufacturing a positive electrode precursor with orientation when there is no concentration gradient by allowing orientation realizable by a conventional batch reactor to be realized by a flow reactor.

DETAILED DESCRIPTION OF THE EMBODIMENTS

Exemplary embodiments of the present invention will now be described in detail. However, these are presented as examples, and the present invention is not limited thereto and is only defined by the scope of the claims to be described later.

In general, to manufacture an oriented positive electrode precursor, a precursor is generated by using a core solution mainly forming an internal composition and a shell solution mainly forming an external composition.

In detail, the concentration of metal ions is changed by partly generating an internal portion of the precursor with the core solution and inputting the shell solution to the core solution, and an external portion of the precursor is generated by inputting a metal ion solution in the changed concentration to a reactor.

In this instance, a concentration gradient is formed from the interior of the precursor toward the exterior thereof, showing a characteristic of orientation. Conventional art used a process for realizing a concentration gradient in the precursor so as to impart orientation to the precursor. For this reason, it had a drawback of only applying a batch-type reaction when attempting to realize the positive electrode material with orientation. The present invention proposes a method for manufacturing an oriented positive electrode material by changing not a concentration gradient but a processing condition.

Regarding a basic idea on the present invention, a principle of an orientation realizing mechanism includes: simplifying a dissolution phenomenon of ions in a solution based on nickel, manganese, and cobalt and not the concentration gradient with a concept of supersaturation, applying the same to an actual process, and acquiring an oriented positive electrode material.

In general, when a co-precipitation area with no complexing agent is calculated in the case of manganese, cobalt, and nickel ions used in the ternary positive electrode material, precipitation occurs at pH 7.5 in the case of manganese ions, at pH 9.2 in the case of cobalt ions, and at equal to or greater than pH 9.6 in the case of nickel ions.

However, in the presence of ammonia, which occurs in the actual co-precipitation condition, precipitation happens in a pH range that is much higher than the above-proposed value of pH in the case of nickel or cobalt that may be combined with ammonia. This is because the nickel and cobalt ions that may configure a complex with ammonia have a very high formation constant for indicating stability of the complex.

A complex compound combined with ammonia becomes very high, compared to the co-precipitation range when there is no ammonia.

In addition, regarding complex formation constants of the cobalt and nickel ions that may configure a complex with ammonia, the complex formation constants of the two materials are substantially different from each other, and in detail, the constant shows the value of 5×10⁴ in the case of Co(NH₃)₆ ²⁺ that is a complex of the cobalt ions, and the constant shows the value of 2×10⁸ in the case of Ni(NH₃)₆ ²⁺ that is a complex of the nickel ions, so the complex of the nickel ions exists in a more stable way.

For the above-noted reason, Ni(NH₃)₆ ²⁺ undergoes precipitation in a higher pH range than Co(NH₃)₆ ²+, and the complex of the nickel ions frequently remains in a supernatant after a reaction in the case of co-precipitation driving.

Therefore, when the solubility of the metal ammonia complex compound is reversely estimated based on the above-noted precipitation phenomenon, the nickel complex compound ions (Ni(NH₃)₆ ²⁺) may be considered to have the highest solubility, and the cobalt complex compound ions (Co(NH₃)₆ ²⁺) may then be determined to have high solubility in a same driving condition of the process for manufacturing a ternary positive electrode precursor.

The manganese ions may not form a complex, so the solubility may be relatively very much lower than the nickel and cobalt ions. That is, in the same processing conditions such as concentration and pH by which the ternary positive electrode precursor is manufactured, an agitation speed, and a temperature, the solubility of the metal ions in the reactor may be considered to be increased as the composition of nickel in a precursor inflow solution increases, and the solubility of the metal ions may be considered to be reduced as the composition of manganese increases.

The major idea of the present invention is to analyze the conventional art according to understanding on the above-described concept and suggest a method for and realizing new orientation.

The conventional orientation realizing method is to realize the concentration gradient of the precursor, and the core solution used in an initial stage has a high nickel concentration, while the solution using a shell solution includes a large amount of manganese ions, so it is found that the solubility of the metal ions is low. That is, regarding the conventional method for realizing a precursor with orientation, the solubility of metal ions is very high in a center of the precursor, and the solubility of metal ions is gradually lowered toward the outside thereof.

The conventional art also uses a batch reactor, so the concentration of ions in the initial solution existing in the reactor is gradually lowered as the reaction progresses, and as a result, the conventional orientation realizing method may be deemed to be a driving method for maintaining the concentration of metal ions in the solution at less than a supersaturated state from start to end and preventing steep precipitation or crystal nuclei from being generated in a middle of the reaction.

To summarize such points and make a determination, the orientation realizing mechanism according to prior art may be analyzed, by the concept of the present invention, to be a method for manufacturing a precursor using a self-assembly phenomenon to the maximum by growing crystal while suppressing precipitation and nucleation in a maximum way.

Therefore, the present invention proposes a method for realizing orientation in a flow reactor based on the above-noted mechanism.

The present invention confirms that it is possible to manufacture a positive electrode material with orientation according to a process variable by using the conventional precursor manufacturing mechanism. That is, when co-precipitation driving is progressed in the condition of suppressing nucleation by controlling the process variable, orientation may be imparted in the situation of no concentration gradient in the influent according to a driving time.

The process variables in the precursor co-precipitation process include a reactor agitation speed, an inflow amount of ammonia against metal ions, a value of pH in the reactor, a temperature inside the reactor, and a reactor residence time.

An increase of the agitation speed is determined to impart orientation. In detail, it is found that, when the agitation speed of the reactor is a linear velocity that is equal to or greater than 3 m/s and equal to or less than 15 m/s, the precursor with orientation is acquired. The agitation speed with the above-noted velocity may be generally realized to be in a range that is equal to or greater than 80 rpm in a 1 cubic meter-level Taylor reactor.

It is found that orientation is shown as a use of ammonia that is a complexing agent input to a metal ion material increases. In the present invention, the precursor with orientation is obtained when the input flow of ammonia against metal ions is 1:0.95 to 1:1.5 as a molar ratio. In detail, the precursor with the best orientation may be obtained when it is 1:1.1 to 1:1.2.

As the temperature of the reactor lowers, the nucleation is suppressed and orientation is then obtained. The orientation may be obtained at 25 to 55° C., and the precursor with the best orientation is obtainable at 30 to 45° C.

It is the most advantageous to minimize a reactor residence time. Regarding the present reactor, the precursor with orientation is obtained when the residence time is 30 min to 4 h, and in detail, the best orientation is obtained when it is 30 min to 1 h.

Based upon such the idea, the orientation is realized by changing the agitation speed of the reactor, the ratio of ammonia, the reaction temperature, and the residence time. The above-noted orientation realizing method is applicable to a Taylor reactor and a batch reactor for manufacturing a positive electrode precursor as well as the continuous tank reactor.

Desired exemplary embodiments of the present invention, a comparative example compared thereto, and estimated examples thereof will now be described. However, the exemplary embodiments to be described below are examples of the present invention, and the present invention is not limited thereto.

EXPERIMENTAL EXAMPLE Manufacturing a Positive Active Material

A positive electrode precursor is manufactured by applying a 50 liter Couette-Taylor flow reactor.

Regarding the initial condition in the reactor, pH is adjusted to be 10.7 by using a solution that is a mixture of 25 wt % caustic soda and 28 wt % ammonia at a weight percent of 85:15. NaOH is then added according to a reactor driving pH. To inject a reactant, a metal sulfate solution of a 2.5M concentration mixed with a nickel sulfate, a cobalt sulfate, and a manganese sulfate at a molar ratio of 88:9.5:2.5 is continuously added.

The temperature inside the reactor is changed according to respective conditions as expressed in the tables below, and driving is performed while maintaining the temperature. The mole flow (mol/min) of ammonia against the mole flow (mol/min) of the metal sulfate solution is also changed according to the reference given in the tables. Co-precipitation is performed by adjusting pH to be in a targeted range by use of NaOH.

Tests other than the change of agitation speed have a set condition of driving a Taylor reactor with the linear velocity of 11.0 m/s and a residence time of 1 h. The manufactured co-precipitation precursor is obtained, an ICP analysis is performed, and a calcination process is performed for 15 h at 750° C. with the molar ratio of LiOH with the composition of 1.03 against metal to thus obtain a final positive electrode material.

Electrochemical Characteristic Estimating Method

An electrochemical estimation is performed by using a CR2032-type coin cell. A slurry for manufacturing an electrode plate has the ratio of positive electrode:conductive material (Denka black):binder (PVDF, KF1100)=96.5:2.0:1.5 wt %, and viscosity of the slurry is adjusted by adding NMP (N-methyl-2-pyrrolidone) so that a solid amount may be about 30%.

The manufactured slurry is coated on a foil of Al that is 15 μm thick by using a doctor blade, and is then dry rolled. An electrode loading amount is 14.6 mg/cm², and rolling density is 3.1 g/cm³.

The electrolyte solution generated by adding 1.5% of VC to a 1M LiPF6 in EC:DMC:EMC=3:4:3 (vol %) is used, a coin cell is manufactured by using a

PP separation film and a lithium cathode (200 μm, Honzo metal), an aging process is performed at room temperature for 10 h, and a charging and discharging test is performed.

Capacity estimation is performed with 200 mAh/g as a reference capacity, and an applied charging and discharging condition includes a CC/CV of 2.5 to 4.25 V and a cut-off of 1/20 C.

Initial capacity performs a 0.2C charging/0.2 C discharging after a 0.1 C charging/0.1 C discharging.

An output characteristic is obtained by measuring discharging capacity while increasing a C-rate at 0.1 C/0.2 C/0.5 C/1 C/1.3 C/1.5 C/2 C, and a high-temperature cycle lifespan characteristic is measured thirty times at a high temperature of 45° C. in the 0.3 C charging/0.3 C discharging condition.

Orientation Analysis Method

To analyze orientation of positive electrode material powder particles, several tens to several hundreds of positive electrode material powder particles are fixed to a polymer resin and a mounting process is performed. After the mounting process is progressed, a polishing process is performed to a dried sample for a first time by using sandpaper, and the sample is transferred to an ion milling device so that a secondary surface process is performed thereto. When a cross-sectional image of the powder is observed to find that a hemispherical positive electrode material (a circular cross-section) is acquired after the ion milling process is finished, an operation for processing the cross-section of the positive electrode material is finished. The sample of which the cross-section is processed is moved to EBSD equipment and its orientation is analyzed. The orientation in directions of [001], [120], and [210] is analyzed with reference to a misorientation angle of +/−30 degrees. A reference structure uses a hexagonal structure, and a pole figure is acquired with respect to an ND axis and an RD axis.

Estimation Example 1: Manipulating Variables of [a Total Number of Moles of Metal Ions in a Metal Salt Aqueous Solution: a Number of Moles of Ammonia], and Controlling Other Variables Within a Range of a Comparative Example

As expressed in Table 1 to Table 4, one variable is given, and other variables are controlled. The results are given in Table 1 below.

As can be known from Table 1 to Table 4, a property of the positive electrode material is excellent in the range of 1:0.95 to 1:1.5. Further preferably, it is excellent in the range of 1:1.1 to 1:1.2.

TABLE 1 EBSD analysis result with less than 30 degrees of misorientation angle (Δg) Direction of Sphericity Density Manipulating Direction of Direction of Direction of [120] + l/w (g/cc) variables [001] [210] [120] [210] (Long axis 25° C., Molar ratio with with with with diameter/short 25° C. 20 kN of metal respect respect respect respect axis diameter of Tap Roll No. ions:ammonia to ND axis to ND axis to ND axis to ND axis cross-section) density density A01 1:0.65 15 40 45 85 1.81 1.3 1.8 A02 1:0.75 18 41 41 82 1.72 1.6 2.2 A03 1:0.85 19 37 44 81 1.51 1.8 2.5 A04 1:0.95 22 37 41 78 1.46 2.2 3.0 A05 1:1.00 24 37 39 76 1.23 2.3 3.1 A06 1:1.10 29 35 36 71 1.13 2.5 3.4 A07 1:1.15 32 34 34 68 1.13 2.6 3.5 A08 1:1.20 34 31 35 66 1.02 2.5 3.4 A09 1:1.25 34 32 35 67 1.02 2.1 2.9 A10 1:1.35 34 33 34 67 1.03 2.0 2.7 A11 1:1.45 33 32 35 67 1.04 1.8 2.5 A12 1:1.5  34 31 36 67 1.03 1.7 2.3 A13 1:1.55 33 33 34 67 1.06 1.6 2.3 A14 1:1.65 32 33 35 68 1.09 1.6 2.3 A15 1:1.75 30 34 36 70 1.0 1.6 2.2

TABLE 2 EBSD analysis result with misorientation angle (Δg) of less than 30 degrees Density Manipulating Direction of Direction of Direction of Direction of (g/cc) variables [001] [210] [120] [120] + 25° C., Molar ratio with with with [210] 25° C. 20 kN of metal respect respect respect with respect Sphericity Tap Roll No. ions:ammonia to RD axis to RD axis to RD axis to RD axis l/w density density A01 1:0.65 63 20 18 38 1.81 1.3 1.8 A02 1:0.75 49 24 27 51 1.72 1.6 2.2 A03 1:0.85 38 27 35 62 1.51 1.8 2.5 A04 1:0.95 29 28 43 71 1.46 2.2 3.0 A05 1:1.00 25 29 46 75 1.23 2.3 3.1 A06 1:1.10 18 32 50 82 1.13 2.5 3.4 A07 1:1.15 15 33 52 85 1.13 2.6 3.5 A08 1:1.20 13 35 52 87 1.02 2.5 3.4 A09 1:1.25 14 34 52 86 1.02 2.1 2.9 A10 1:1.35 15 35 50 85 1.03 2.0 2.7 A11 1:1.45 14 37 49 86 1.04 1.8 2.5 A12 1:1.5  14 38 47 86 1.03 1.7 2.3 A13 1:1.55 14 34 52 86 1.06 1.6 2.3 A14 1:1.65 13 33 54 87 1.09 1.6 2.3 A15 1:1.75 15 32 53 85 1.03 1.6 2.2

TABLE 3 Manipulating variables Molar ratio of metal No. ions:ammonia D10 D25 D50 D75 D90 A01 1:0.65 8.9 10.0 11.7 13.8 16.3 A02 1:0.75 8.4 9.4 11.0 13.0 15.3 A03 1:0.85 7.7 8.7 10.2 12.0 14.1 A04 1:0.95 12.6 14.1 16.5 19.5 23.0 A05 1:1.00 12.5 14.1 16.4 19.4 22.9 A06 1:1.10 12.8 14.4 16.8 19.8 23.3 A07 1:1.15 12.7 14.3 16.7 19.7 23.2 A08 1:1.20 12.9 14.5 17.0 20.0 23.6 A09 1:1.25 12.7 14.2 16.6 19.6 23.1 A10 1:1.35 12.4 13.9 16.3 19.2 22.6 A11 1:1.45 12.1 13.6 16.1 8.8 22.2 A12 1:1.5  11.9 13.3 16.0 18.4 21.7 A13 1:1.55 9.7 10.9 12.7 15.0 17.7 A14 1:1.65 9.4 10.6 12.4 14.6 17.2 A15 1:1.75 9.0 10.1 11.9 14.0 16.5

TABLE 4 Characteristics Characteristics of 25 OR 30° C. of 45° C. Capacity Capacity Capacity Initial maintaining maintaining maintaining discharging 30 cycle rate (%) 100 cycle rate (%) rate (%) capacity Initial discharging after 30 discharging after 100 after 100 No. @0.2 C efficiency capacity cycles capacity cycles cycles A01 192.3 84.0 175.4 85 149.1 78 37 A02 198.8 86.8 188.2 89 167.4 85 45 A03 201.0 87.8 189.6 91 172.5 92 80 A04 205.4 89.7 196.5 97 190.6 95 85 A05 206.7 90.3 196.7 97 190.8 95 86 A06 207.6 90.7 196.5 98 192.5 95 86 A07 208.2 90.8 197.1 98 193.1 96 86 A08 208.7 91.2 197.7 98 193.7 96 85 A09 209.3 91.0 196.5 98 192.6 96 86 A10 210.2 91.1 196.7 98 192.8 96 86 A11 211.3 91.8 196.4 97 190.5 95 85 A12 211.2 91.4 195.8 97 190.0 95 85 A13 211.4 90.6 193.1 95 167.9 87 76 A14 210.7 89.7 189.7 90 153.6 81 65 A15 210.8 88.0 180.1 88 117.1 65 37

Estimation Example 2: Manipulating Reaction pH Variable, and Controlling Other Variables Within a ange of Comparative Example

As expressed in Table 5 to Table 8, one variable is given, and other variables are controlled. The results are expressed in Table 5 to Table 8.

As can be known from Table 5 to Table 8, the pH range of 10.5 to 12 is found to be excellent.

TABLE 5 EBSD analysis result with misorientation angle (Δg) of less than 30 degrees Direction of Sphericity Direction of Direction of Direction of [120] + l/w Density [001] [210] [120] [210] (Long axis (g/cc) Manipulating with with with with diameter/short 25° C. variables respect respect respect respect axis diameter of Tap

No. Processing pH to ND axis to ND axis to ND axis to ND axis cross-section) density

B01 9.0 32 33 35 68 1.12 1.66

B02 9.5 33 33 34 67 1.13 1.76

B03 10.0 34 31 36 67 1.12 1.87

B04 10.5 33 32 35 67 1.09 2.0

B05 11.0 34 31 35 66 1.08 2.5

B06 11.5 29 35 36 71 1.17 2.5

B07 12.0 22 37 41 74 1.36 2.3

B08 12.5 18 41 41 82 1.73 1.6

indicates data missing or illegible when filed

TABLE 6 EBSD analysis result with misorientation angle (Δg) of less than 30 degrees Direction of Density Direction of Direction of Direction of [120] + (g/cc) [001] [210] [120] [210] 25° C., Manipulating with with with with 25° C. 20 kN variables respect respect respect respect Sphericity Tap Roll No. Processing pH to RD axis to RD axis to RD axis to RD axis l/w density density B01 9.0 15 32 53 85 1.12 1.66 2.3 B02 9.5 15 38 47 85 1.13 1.76 2.3 B03 10.0 14 34 52 87 1.12 1.87 2.4 B04 10.5 14 34 52 86 1.09 2.0 3.0 B05 11.0 13 35 52 87 1.08 2.5 3.4 B06 11.5 18 32 50 82 1.17 2.5 3.4 B07 12.0 22 31 47 78 1.36 2.3 3.1 B08 12.5 49 24 27 51 1.73 1.6 2.2

TABLE 7 Manipulating variables No. Processing pH D10 D25 D50 D75 D90 B01 9.0 9.1 10.2 11.9 14.1 16.6 B02 9.5 12.0 13.4 15.7 18.5 21.8 B03 10.0 12.5 14.0 16.4 19.3 22.7 B04 10.5 12.8 14.3 16.7 19.7 23.2 B05 11.0 13.0 14.6 17.1 20.1 23.7 B06 11.5 12.6 14.2 16.5 19.5 23.0 B07 12.0 12.7 14.2 16.6 19.6 23.1 B08 12.5 8.5 9.5 11.1 13.1 15.4

TABLE 8 Characteristics Characteristics of 25 OR 30° C. of 45° C. Capacity Capacity Capacity Initial maintaining maintaining maintaining discharging 30 cycle rate (%) 100 cycle rate (%) rate (%) capacity Initial discharging after 30 discharging after 100 after 100 No. @0.2 C efficiency capacity cycles capacity cycles cycles B01 192.3 84.0 175.4 85 149.2 78 44 B02 198.8 86.8 188.2 89 167.5 85 65 B03 201.0 87.8 189.6 91 172.6 92 76 B04 205.4 89.7 196.5 97 190.6 95 83 B05 206.7 90.3 196.7 97 190.8 95 84 B06 208.7 90.8 196.5 97 192.6 96 85 B07 208.2 91.2 197.1 98 193.2 96 85 B08 209.3 92.1 181.0 88 117.0 65 37

Estimation Example 3: Manipulating Residence Time Variable of Metal Salt Solution, and Controlling Other Variables Within the Range of Comparative Example

As expressed in Table 9 to Table 12, one variable is given, and other variables are controlled. The results are expressed in Table 9 to Table 12.

As can be found from Table 9 to Table 12, the residence time in the range of 30 minutes to 4 hours is found to be excellent.

TABLE 9 EBSD analysis result with misorientation angle (Δg) of less than 30 degrees Direction of Sphericity Density Direction of Direction of Direction of [120] + l/w (g/cc) Manipulating [001] [210] [120] [210] (Long axis 25° C. variables with with with with diameter/short 25° C. 20 kN Residence respect respect respect respect axisdiameter of Tap Roll No. time to ND axis to ND axis to ND axis to ND axis cross-section) density density C01 15 min 32 34 35 68 1.31 1.3 2.3 C02 30 min 33 33 34 67 1.02 1.7 2.3 C03 1 h 34 31 36 67 1.01 1.8 2.5 C04 2 h 34 31 35 66 1.01 2.4 3.5 C05 3 h 29 35 36 71 1.09 2.2 3.4 C06 4 h 19 37 44 71 1.21 2.4 3.4 C07 6 h 18 41 41 82 1.22 2.5 3.4 C08 8 h 19 40 41 81 1.27 2.5 3.5

TABLE 10 EBSD analysis result with misorientation angle (Δg) of Density less than 30 degrees RD axis (g/cc) Manipulating RD axis RD axis RD axis respect 25° C., variables respect respect respect [120] + 25° C. 20 kN Residence [001] [210] [120] [210] Sphericity Tap Roll No. time direction direction direction direction l/w density density C01 15 min 15 32 53 85 1.31 1.3 2.3 C02 30 min 14 34 52 86 1.02 1.7 2.3 C03 1 h 15 38 47 85 1.01 1.8 2.5 C04 2 h 14 34 52 86 1.01 2.4 3.5 C05 3 h 25 29 46 75 1.09 2.2 3.4 C06 4 h 38 27 35 62 1.21 2.4 3.4 C07 6 h 49 24 27 51 1.22 2.5 3.4 C08 8 h 50 20 30 50 1.27 2.5 3.5

TABLE 11 Manipulating variables No. Residence time D10 D25 D50 D75 D90 C01 15 min 9.1 10.0 11.8 13.9 16.4 C02 30 min 9.7 10.8 12.6 14.9 17.6 C03 1 h 12.1 13.5 15.8 18.7 22.1 C04 2 h 12.8 14.4 16.9 19.9 23.5 C05 3 h 15.4 17.3 20.3 23.9 28.2 C06 4 h 14.8 16.6 19.4 22.9 27.0 C07 6 h 14.1 15.9 18.6 21.9 25.8 C08 8 h 13.5 15.1 17.7 20.9 24.7

TABLE 12 Characteristics Characteristics of 25 OR 30° C. of 45° C. Capacity Capacity Capacity maintaining maintaining maintaining 30 cycle rate (%) 100 cycle rate (%) rate (%) Residence Initial discharging after 30 discharging after 100 after 100 No. time efficiency capacity cycles capacity cycles cycles C01 15 min 91.4 189.7 88 117.0 65 37 C02 30 min 91.8 196.4 97 188.4 95 86 C03 1 h 91.0 196.5 98 188.5 96 86 C04 2 h 91.2 197.7 98 193.6 96 85 C05 3 h 89.7 196.7 97 190.8 95 83 C06 4 h 87.8 189.6 91 172.4 92 76 C07 6 h 86.8 188.2 89 167.3 85 65 C08 8 h 84.0 175.4 85 149.0 78 44

Estimation Example 4: Manipulating Agitation Speed Variable, and Controlling Other Variables Within the Range of Comparative Example

As expressed in Table 13 to Table 16, one variable is given, and other variables are controlled. The results are expressed in Table 13 to Table 16.

As can be known from Table 13 to Table 16, the agitation speed in the range of 80 to 200 rpm is found to be excellent.

TABLE 13 EBSD analysis result with misorientation angle (Δg) of less than 30 degrees Direction of Sphericity Density Direction of Direction of Direction of [120] + l/w (g/cc) Manipulating [001] [210] [120] [210] (Long axis 25° C., variables with with with with diameter/short 25° C. 20 kN Agitation respect respect respect respect axis diameter of Tap Roll No. speed to ND axis to ND axis to ND axis to ND axis cross-section) density density D01 30 15 40 45 85 1.83 1.6 2.1 D02 50 18 41 41 82 1.52 1.8 2.4 D03 80 29 35 36 71 1.12 2.5 3.4 D04 100 34 31 35 66 1.07 2.5 3.4 D05 200 34 32 35 67 1.07 2.6 3.4 D06 300 18 41 41 82 1.09 2.3 3.3

TABLE 14 EBSD analysis result with misorientation angle (Δg) of less than 30 degrees Density Direction of Direction of Direction of Direction of (g/cc) Manipulating [001] [210] [120] [120] + 25° C., variables with with with [210] 25° C. 20 kN Agitation respect respect respect with respect Sphericity Tap Roll No. speed to RD axis to RD axis to RD axis to RD axis l/w density density D01 30 63 20 18 38 1.83 1.6 2.1 D02 50 49 24 27 51 1.52 1.8 2.4 D03 80 23 31 46 77 1.12 2.5 3.4 D04 100 18 32 50 82 1.07 2.5 3.4 D05 200 15 38 47 85 1.07 2.6 3.4 D06 300 38 27 35 62 1.09 2.3 3.3

TABLE 15 Manipulating variables No. Processing pH D10 D25 D50 D75 D90 D01 30 8.6 10.2 11.9 14.0 16.5 D02 50 7.8 8.9 10.4 12.2 14.3 D03 80 13.0 14.6 17.0 20.0 23.5 D04 100 12.9 14.5 16.9 19.9 23.5 D05 200 13.1 14.7 17.2 20.2 23.8 D06 300 9.2 10.3 12.1 14.2 16.7

TABLE 16 Characteristics Characteristics of 25 OR 30° C. of 45° C. Capacity Capacity Capacity Initial maintaining maintaining maintaining discharging 30 cycle rate (%) 100 cycle rate (%) rate (%) capacity Initial discharging after 30 discharging after 100 after 100 No. @0.2 C efficiency capacity cycles capacity cycles cycles D01 198.8 86.8 188.2 89 167.4 85 65 D02 201.0 87.8 189.6 91 172.5 92 76 D03 207.6 90.7 196.5 98 192.5 95 85 D04 208.2 90.8 197.1 98 193.1 95 85 D05 208.7 91.2 197.7 98 193.7 96 85 D06 209.3 88.0 196.7 88 117.1 65 37

Estimation Example 5: Manipulating Reaction Temperature Variable, and Controlling Other Variables Within the Range of Comparative Example

As expressed in Table 17 to Table 20, one variable is given, and other variables are controlled. The results are expressed in Table 17 to Table 20.

As can be known from Table 17 to Table 20, the reaction temperature in the range of 30 to 50° C. (in detail, 30 to 45° C.) is found to be excellent.

TABLE 17 EBSD analysis result with misorientation angle (Δg) of less than 30 degrees Direction of Sphericity Density Direction of Direction of Direction of [120] + l/w (g/cc) Manipulating [001] [210] [120] [210] (Long axis 25° C., variable with with with with diameter/short 25° C. 20 kN Reaction respect respect respect respect axis diameter of Tap Roll No. temperature to ND axis to ND axis to ND axis to ND axis cross-section) density density E01 25 32 33 35 68 1.23 1.8 2.6 E02 30 34 31 36 67 1.17 2.3 3.4 E03 35 34 32 35 67 1.09 2.4 3.4 E04 40 29 35 36 71 1.06 2.6 3.5 E05 45 24 37 39 76 1.03 2.6 3.5 E06 50 19 37 44 81 1.11 2.6 3.4 E07 60 15 40 45 85 1.67 2.5 3.2

TABLE 18 EBSD analysis result with misorientation angle (Δg) of less than 30 degrees Density Direction of Direction of Direction of Direction of (g/cc) Manipulating [001] [210] [120] [120] + 25° C., variables with with with [210] 25° C. 20 kN Reaction respect respect respect with respect Sphericity Tap Roll No. temperature to RD axis to RD axis to RD axis to RD axis l/w density density E01 25 15 32 53 85 1.23 1.8 2.6 E02 30 14 34 52 86 1.17 2.3 3.4 E03 35 14 35 50 85 1.09 2.4 3.4 E04 40 15 33 52 85 1.06 2.6 3.5 E05 45 18 32 50 82 1.03 2.6 3.5 E06 50 29 28 43 71 1.11 2.6 3.4 E07 60 38 27 35 62 1.67 2.5 3.2

TABLE 19 Manipulating variables No. Reaction temperature D10 D25 D50 D75 D90 E01 25 3.7 4.2 5.1 6.0 7.0 E02 30 5.0 5.7 6.8 8.1 9.5 E03 35 7.6 8.6 10.2 11.9 14.1 E04 40 12.5 14.0 16.4 19.4 23.0 E05 45 12.7 14.3 16.7 19.7 23.2 E06 50 12.6 14.2 16.6 19.6 23.3 E07 60 6.3 7.1 8.5 10.0 11.8

TABLE 20 Characteristics Characteristics of 25 OR 30° C. of 45° C. Capacity Capacity Capacity Initial maintaining maintaining maintaining discharging 30 cycle rate (%) 100 cycle rate (%) rate (%) capacity Initial discharging after 30 discharging after 100 after 100 No. @0.2 C efficiency capacity cycles capacity cycles cycles E01 211.3 91.8 196.4 97 149.1 78 77 E02 211.2 91.2 195.8 97 186.0 95 85 E03 209.3 91.0 196.5 98 188.6 96 86 E04 210.2 89.7 196.5 97 190.6 95 84 E05 209.7 91.0 196.6 98 188.7 96 86 E06 206.7 87.3 189.6 91 179.6 89 81 E07 195.4 85.7 181.7 86 167.5 81 69

Estimation Example 6: Final Poduct Manufacturing Tests (Comparative Example and exemplary embodiment)

An exemplary embodiment (EE) applies a process variable that is in an optimized area and a comparative example (CE) performs a test on a case that is outside the optimized area and showing no orientation.

TABLE 21 Molar ratio Residence Agitation Reaction metal Reaction time speed temperature No. ions:ammonia pH (h) (rpm) (° C.) EE1  1:1.10 11.0 1.0 100 45 EE2 1:1.2 11.0 1.0 100 45 EE3 1:1.1 10.5 1.0 100 45 EE4 1:1.1 11.0 0.5 100 45 EE6 1:1.1 11.0 1.0 200 45 EE7 1:1.1 11.0 1.0 100 35 CE1  1:0.85 12.5 4.0 50 60

TABLE 22 EBSD analysis result with misorientation angle (Δg) of less than 30 degrees Direction of Sphericity Density Direction of Direction of Direction of [120] + l/w (g/cc) [001] [210] [120] [210] (Long axis 25° C., with with with with diameter/short 25° C. 20 kN Manipulating respect respect respect respect axis diameter of Tap roll No. variables to ND axis to ND axis to ND axis to ND axis cross-section) density density EE1 Orientation 29 35 36 71 1.13 2.5 3.4 improving condition EE2 Ammonia 34 32 35 67 1.03 2.4 3.2 increase EE3 pH reduction 32 34 34 68 1.06 2.3 3.2 EE4 Residence 33 33 34 67 1.02 2.1 3.2 time reduction EE6 Agitation 34 31 35 66 1.07 2.4 3.5 speed increase EE7 Reaction 34 32 35 67 1.17 2.1 3.1 temperature reduction CE1 Orientation 15 40 45 85 1.67 1.3 2.3 suppressing condition

TABLE 23 EBSD analysis result with misorientation angle (Δg) of less than 30 degrees Density Direction of Direction of Direction of Direction of (g/cc) [001] [210] [120] [120] + 25° C., with with with [210] 25° C. 20 kN Manipulating respect respect respect with respect Sphericity Tap Roll No. variables to RD axis to RD axis to RD axis to RD axis l/w density density EE1 Orientation 18 32 50 82 1.13 2.5 3.4 improving condition EE2 Ammonia 14 34 52 86 1.03 2.4 3.2 increase EE3 pH reduction 15 33 52 85 1.06 2.3 3.2 EE4 Residence 14 37 49 86 1.02 2.1 3.2 time reduction EE6 Agitation 13 35 52 87 1.07 2.4 3.5 speed increase EE7 Reaction 14 37 49 86 1.17 2.1 3.1 temperature reduction CE1 Orientation 63 20 18 38 1.67 1.3 2.3 suppressing condition

TABLE 24 Characteristics Characteristics of 25 OR 30° C. of 45° C. Capacity Capacity Capacity Initial maintaining maintaining maintaining discharging 30 cycle rate (%) 100 cycle rate (%) rate (%) capacity Initial discharging after 30 discharging after 100 after 100 No. @0.2 C efficiency capacity cycles capacity cycles cycles EE1 208.7 91.2 197.7 98 193.7 96 85 EE2 209.3 91.0 196.5 98 192.6 96 86 EE3 210.2 91.1 196.7 98 192.8 96 86 EE4 211.4 90.6 193.1 95 179.8 93 84 EE6 207.6 90.7 196.5 98 192.5 95 86 EE7 213.6 92.8 198.3 98 194.5 97 89 CE1 210.8 88.0 180.1 88 117.1 65 37

The present invention is not limited to the exemplary embodiments and may be produced in various forms, and it will be understood by those skilled in the art to which the present invention pertains that exemplary embodiments of the present invention may be implemented in other specific forms without modifying the technical spirit or essential features of the present invention. Therefore, it should be understood that the aforementioned exemplary embodiments are illustrative in terms of all aspects and are not limited. 

1. A positive active material which is a lithium composite metal oxide including nickel, cobalt, and manganese, and has orientation in a direction of with respect to an ND axis that is equal to or greater than 29% in the case of an EBSD analysis with a misorientation angle (Δg) that is equal to or less than 30 degrees. 2-6. (canceled)
 7. The positive active material of claim 1, wherein the lithium composite metal oxide being manufactured according to a co-precipitation method, in this instance, [a total number of moles of metal ions in a metal salt aqueous solution: a number of moles of ammonia] being controlled.
 8. The positive active material of claim 1, wherein the lithium composite metal oxide being manufactured according to a co-precipitation method, and a pH range being controlled in this instance.
 9. The positive active material of claim 1, wherein the lithium composite metal oxide being manufactured according to a co-precipitation method, and a residence time in a reactor of a metal aqueous solution being controlled in this instance.
 10. The positive active material of claim 1, wherein the lithium composite metal oxide being manufactured according to a co-precipitation method, and an agitation speed in a co-precipitation reactor being controlled in this instance.
 11. The positive active material of claim 1, wherein the lithium composite metal oxide being manufactured according to a co-precipitation method, and a reaction temperature in a co-precipitation reactor being controlled in this instance. 12-18. (canceled)
 19. A method for manufacturing a positive active material, comprising: inducing a co-precipitation reaction while agitating a metal salt aqueous solution including a nickel salt, a manganese salt, and a cobalt salt, ammonia, and caustic soda in a reactor; obtaining a composite metal hydroxide precursor including nickel, cobalt, and manganese by the inducing of a co-precipitation reaction; and obtaining a lithium composite oxide by mixing the composite metal hydroxide and a lithium raw material and baking the same, wherein, in the inducing of a co-precipitation reaction, a number of moles of ammonia against a total number of moles of metal ions in the metal salt aqueous solution is 1:0.95 to 1:1.5 [the total number of moles of metal ions in the metal salt aqueous solution: the number of moles of ammonia].
 20. The method of claim 19, wherein the inducing of a co-precipitation reaction includes continuously inputting the metal salt aqueous solution into the reactor, injecting the ammonia by a fixed quantity, and inputting the caustic soda so as to maintain pH in the reactor.
 21. The method of claim 19, wherein in the inducing of a co-precipitation reaction, a number of moles of the ammonia injected by a fixed quantity against a total number of moles of metal ions of the continuously input metal salt aqueous solution is 1:1.1 to 1:1.2 [a total number of moles of metal ions of the continuously input metal salt aqueous solution: a number of moles of ammonia injected by a fixed quantity].
 22. The method of claim 19, wherein in the inducing of a co-precipitation reaction, a temperature in the reactor is 25 to 55° C.
 23. The method of claim 19, wherein in the inducing of a co-precipitation reaction, a temperature in the reactor is 30 to 45° C.
 24. The method of claim 19, wherein in the inducing of a co-precipitation reaction, a residence time of the metal salt solution in the reactor is 30 minutes to 4 hours.
 25. The method of claim 19, wherein in the inducing of a co-precipitation reaction, a residence time of the metal salt solution in the reactor is 30 minutes to 1 hour.
 26. The method of claim 19, wherein in the inducing of a co-precipitation reaction, pH in the reactor is maintained at a range of 10.5 to 12.0.
 27. The method of claim 19, wherein in the inducing of a co-precipitation reaction, an agitation speed of metal salt aqueous solution, ammonia, and caustic soda in the reactor is 3 m/s to 15 m/s as a linear velocity.
 28. The method of claim 19, wherein in the inducing of a co-precipitation reaction, an agitation speed of a metal salt aqueous solution, ammonia, and caustic soda in the reactor is 80 to 200 rpm as a rotation speed.
 29. The method of claim 19, wherein in the inducing of a co-precipitation reaction, [a total number of moles of metal ions of a continuously input metal salt aqueous solution: a number of moles of ammonia injected by a fixed quantity] is 1:1.1 to 1:1.2, pH is the reactor is maintained at a range of 10.5 to 12.0, a temperature inside the reactor is 30 to 45° C., a residence time of the metal salt solution in the reactor is 30 minutes to 1 hour, and an agitation speed (a linear velocity) of metal salt aqueous solution, ammonia, and caustic soda in the reactor is 3 msec to 15 m/s.
 30. The method of claim 20, further comprising, before the inducing of a co-precipitation reaction, controlling pH inside the reactor to be 10.5 to 12.0 by inputting a mixed solution of ammonia and caustic soda into the reactor.
 31. A lithium rechargeable battery comprising: a positive electrode including a positive active material of claim 1; a negative electrode; and an electrolyte. 